A PK
polymerization system comprises a
polymerization kettle, an extraction kettle and an extraction
tower, a
raw material inlet, a catalyst inlet and a first
vapor phase outlet are formed in the top of the
polymerization kettle, the
raw material inlet is connected with an
ethylene source, a propylene source, a
carbon monoxide source and an N-methyl pyrrolidone source through a micro-interface reactor, and the catalyst inlet is connected with a catalyst source. The
vapor phase outlet is connected with a first gas-liquid separator, a kettle bottom
discharge port of the polymerization kettle supplies materials to the extraction kettle, the top of the extraction kettle is provided with a desalted water inlet and a second
vapor phase outlet, the second vapor phase outlet is connected with a second gas-liquid separator, and a kettle bottom
discharge port of the extraction kettle supplies materials to the extraction
tower. Gas-phase outlets of the first gas-liquid separator and the second gas-liquid separator flow back to the polymerization kettle through a
recovery compressor and a cooler, liquid-phase outlets of the first gas-liquid separator and the second gas-liquid separator flow back to the polymerization kettle and the extraction kettle respectively, and a
tower bottom
discharge port of the extraction tower discharges PK to the outside. The
continuous production device is simple in structure and low in maintenance cost,
continuous production of the PK
polyketone resin is achieved, and the competitiveness of the
polyketone resin in the
engineering plastic market is improved.